EP0373115A1 - Tête d'extrusion - Google Patents

Tête d'extrusion Download PDF

Info

Publication number
EP0373115A1
EP0373115A1 EP89810907A EP89810907A EP0373115A1 EP 0373115 A1 EP0373115 A1 EP 0373115A1 EP 89810907 A EP89810907 A EP 89810907A EP 89810907 A EP89810907 A EP 89810907A EP 0373115 A1 EP0373115 A1 EP 0373115A1
Authority
EP
European Patent Office
Prior art keywords
melt
passage
extrusion head
head according
mandrel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP89810907A
Other languages
German (de)
English (en)
Other versions
EP0373115B1 (fr
Inventor
Alwin Lehner
Peter Karg
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Soplar SA
Original Assignee
Soplar SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Soplar SA filed Critical Soplar SA
Priority to AT89810907T priority Critical patent/ATE73384T1/de
Publication of EP0373115A1 publication Critical patent/EP0373115A1/fr
Application granted granted Critical
Publication of EP0373115B1 publication Critical patent/EP0373115B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50—Details of extruders
    • B29C48/695—Flow dividers, e.g. breaker plates
    • B29C48/70—Flow dividers, e.g. breaker plates comprising means for dividing, distributing and recombining melt flows
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/30—Extrusion nozzles or dies
    • B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/30—Extrusion nozzles or dies
    • B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B29C48/325—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles being adjustable, i.e. having adjustable exit sections
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/30—Extrusion nozzles or dies
    • B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
    • B29C48/335—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25—Component parts, details or accessories; Auxiliary operations
    • B29C48/92—Measuring, controlling or regulating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92504—Controlled parameter
    • B29C2948/9258—Velocity
    • B29C2948/926—Flow or feed rate
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00—Indexing scheme relating to extrusion moulding
    • B29C2948/92—Measuring, controlling or regulating
    • B29C2948/92819—Location or phase of control
    • B29C2948/92857—Extrusion unit
    • B29C2948/92904—Die; Nozzle zone
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils

Definitions

  • the invention relates to an extrusion head, in particular for the production of preforms for blown containers, e.g. Bottles, made of plastic, with a head body, which has at least one passage, a mandrel arranged in the passage, which has a core at its distal end, a control rod leading through the mandrel for axial adjustment of the core, a mandrel holder with webs which hold the mandrel Hold it in such a way that flow channels for the melt are formed between the wall of the passage and the mandrel.
  • a head body which has at least one passage, a mandrel arranged in the passage, which has a core at its distal end, a control rod leading through the mandrel for axial adjustment of the core, a mandrel holder with webs which hold the mandrel Hold it in such a way that flow channels for the melt are formed between the wall of the passage and the mandrel.
  • Bottles are usually made by means of extrusion heads, tubular preforms, which are then further processed by blow molding.
  • extrusion heads There are two fundamentally different types of extrusion heads to choose from for extruding the preforms, namely heads with lateral flow against the melt, e.g. Quill heads and heads with central flow, the so-called mandrel holder heads.
  • the core of the quill head can be adjusted to adjust the wall thickness, while the mouthpiece of the mandrel holder head.
  • the extrusion device should therefore be able to produce a large number of preforms at the same time.
  • the extrusion head is advantageously fed by a single extruder with plastic melt of a certain temperature.
  • the quill head is relatively simple in construction and therefore relatively cheap.
  • the so-called quill serves for the radial distribution of the melt and the guiding of the control rod for the axial adjustment of the core, which serves to form the cavity in the extruded tube piece. Due to the axial adjustment of the control rod, the core can be adjusted in relation to the mouthpiece by the wall thickness of the hose piece.
  • the quill head it has the disadvantage that the melt flow flowing in from the side is divided into two partial flows through the quill, which then flow together behind the quill. Due to the division of the melt flow by the circular cross section of the quill, unfavorable flow conditions arise in the melt, where thin points can then form in the tube piece at the point where the partial flows flow together.
  • the mandrel holder head is more complicated in construction and therefore usually a little more expensive than the quill head.
  • the mandrel ie the core, which forms the cavity of the preform
  • the body of the head with thin radial webs.
  • These webs can be designed to be fluidly favorable, so that the melt flows cleanly after passing through the webs and there is practically no risk of thin spots forming in the preform.
  • the webs are also designed such that the piece of hose is formed, for example, by two coaxially arranged groups of overlapping partial streams. A possible weak point is always overlapped by a homogeneous layer.
  • mandrel holder heads are offset by the disadvantage that they require a complicated mechanism to adjust the wall thickness of the preform.
  • This adjustment mechanism with which an axial adjustment of the mouthpiece can be accomplished, also offers considerable sealing and stability problems.
  • the adjustment forces are greater than with the quill head. This places tight limits on the designer.
  • Another disadvantage is that it is difficult to build multiple heads with this type of construction.
  • FR-A-1 330 757 shows an extrusion head with a mandrel arranged in a passage.
  • This mandrel has a core at its distal end, which can be adjusted with a control rod leading through the mandrel.
  • a mandrel holder with webs is provided, which hold the mandrel so that flow channels for the melt are formed between the wall of the passage and the mandrel.
  • the disadvantage here is that the melt flow flowing in laterally is irregularly divided into partial flows by the circular cross section of the parts projecting in the melt flow. This creates unfavorable flow conditions, which can result in thin spots in the extruded tubular preform.
  • the extrusion head shown is a single head. Because of the unfavorable flow conditions in the melting channel, this type of construction is also not suitable for the construction of multiple heads, as are desired for the rational use of modern blow molding machines.
  • this is achieved in that an upper part with a melt feed channel arranged therein for charging the passage is arranged on the head body, and a flow divider is provided in the melt feed channel above the passage, which causes the formation of partial flows which cause the control rod in side escape channels can flow around.
  • the melt can be fed in laterally, in which case a deflection into the melt feed channel can take place under favorable flow conditions.
  • the plate then has a common melt feed channel for feeding the passages. This has the advantage that basically a single extruder is sufficient for the simultaneous production of a large number of preforms.
  • melt feed channel with two extruders, it also being possible to feed two different types of melt, for example of different colors, to the melt feed channel.
  • melt feed channel with two extruders
  • two different types of melt for example of different colors
  • the melt feed channel In this way it is also possible to produce bottles that have two different colors, for example colored on the front and transparent on the back.
  • a flow divider is provided above the passage, the formation of clearly defined partial flows is caused, which can flow around the control rod and / or throttle screw in side escape channels.
  • the flow divider ensures a practically optimal flow of the melt; this is in contrast to the well-known quill heads, where the round cross-section of the quill considerably disturbs the flow of the melt.
  • a channel in the control rod for the supply of gas, e.g. Air or liquid to provide for the preform.
  • a throttle screw can be provided at the entrance of the passage. In the case of multiple heads, this makes it possible to match the extrusion speed to one another in the individual extrusion dies, so that preforms of the same length are produced.
  • the throttle screw is expediently designed as a hollow screw through which the control rod passes. This represents a particularly simple and practical construction in which both the control rod and the throttle screw are easily adjustable.
  • the throttle screw can have a practically conical section at the front, which fits into a practically conical extension at the entrance of the flow channel. Such a design results in favorable flow conditions for the melt, fine regulation being possible by means of the throttle screw.
  • the current divider is advantageously designed such that it at least partially surrounds the control rod and the throttle screw.
  • the control rod and throttle screw therefore do not have a detrimental effect on the flow behavior of the melt.
  • the Current divider advantageously has a bow-shaped tip at the front. This tip divides the melt into two practically laminar flows. It is advisable for the flow divider to also end at a point, so that no turbulence occurs.
  • the flow divider advantageously tapers conically from the bottom of the channel in the direction of the passage.
  • the melt is directed into the passage in the axial direction, with virtually no turbulence.
  • the side walls of the last passage to be fed with melt advantageously rise from the channel base.
  • the respective passage advantageously has a trumpet-shaped widening on the inlet side. This ensures that the melt flows optimally into the passage.
  • Fig. 1 shows schematically part of a multiple head for the production of preforms for blown containers. The same construction could also be used for a single head.
  • a passage 13 is formed in the head body 11.
  • a mandrel 15 with webs 17 is held in this passage 13 such that flow channels 19 for the melt are formed between the wall 16 of the passage 13 and the mandrel 15.
  • the formation of the webs 17 can be such as is the case, for example, with a commercially available offset web mandrel extrusion head. Such an arrangement is shown in section in FIG. 6.
  • the mandrel 15 has a downstream, i.e. an adjustable core 21 at the distal end.
  • the mandrel has a cylindrical bore 23 in which a piston-shaped part 25 of the core 21 is slidably mounted.
  • An axially adjustable control rod 27 is used to move the core 21.
  • the adjustment mechanism for the control rod is not shown. It can be formed in the usual way by a screw device.
  • the control rod 27 passes through a coaxial bore 29 of the mandrel 15.
  • the control rod 27 has a channel 31 for supplying air to the preform.
  • the nozzle 33 for producing the tubular preform is formed by the gap between the core 21 and the mouthpiece 35.
  • the melt is supplied via the melt feed channel 37.
  • an extruder (not shown) is connected to the melt feed channel 37.
  • a throttle screw 39 is used to regulate the melt supply into the passage 13. This throttle screw 39 is designed as a hollow screw through which the control rod 27 leads.
  • the melt feed channel 37 is formed in the upper part 41, which is connected to the head body 11, for example with screws (not shown).
  • the configuration of the melt feed channel 37 can be seen in particular from FIGS. 2 to 5. If the extrusion head has a plurality of passages 13, the top 41 can be one for all passages have a common melt feed channel.
  • a flow divider 43 is provided above the passage 13. All flow dividers, except the last 43 '(Fig. 5), are of the same design.
  • the current divider 43 has a bow-shaped tip 45 at the front.
  • the flow divider 43 also has a tip 47 at the rear. From FIGS. 1 and 4 it can be seen that the flow divider tapers conically from the bottom 49 of the melt feed channel 37 in the direction of the passage 13.
  • the surface 48 thus represents a conical surface.
  • the melt feed channel 37 is divided into two side channels 37 'by the flow divider 43.
  • the walls 49 of the side channels 37 ' are relatively thin, so that the deflection of the partial melt flows remains relatively low.
  • melt feed channel 37 is formed entirely in the upper part 41. However, it would also be possible to form the melt feed channel 37 entirely or partially in the head body itself. However, the training described has manufacturing advantages.
  • the last flow divider 43 ' has a somewhat different design than the previous flow divider 43.
  • the front part with the tip 45 is of the same design as previously described. Again, a conical surface 48 is also present. However, the side channels 37 ⁇ extend from the bottom 49 of the melt feed channel 37.
  • the passage 13 has a trumpet-shaped widening 51 on the inlet side.
  • the melt flowing into this expansion 51 can therefore flow downward into the passage 13, provided that the passage 13 is not completely closed with the throttle screw 39 as shown in FIG. 3.
  • the throttle screw 39 has a conical section 53 at the front, which fits into a conical extension 51 at the entrance of the passage 13.
  • the extruder conveys the synthetic resin melt into the melt feed channel 37.
  • the melt flow is divided cleanly by the flow dividers 43.
  • the two partial flows combine again at the rear tip 47 of the flow divider 43.
  • the melt flow thus formed then continues to flow, with further flow dividers possibly repeating the same operation.
  • With each flow divider 43 but also a part of the melt penetrates into the extension 51 and from there further into the passage 13.
  • At the last flow divider 43 ' all the current arriving there flows into the extension 51 of the passage 13.
  • the melt stream flowing into the respective passage 13 then flows around the mandrel 15. Since the webs 17 are thin, they practically do not interfere with the downward flow of the melt stream. Finally, the melt emerges from the nozzle 33 in the form of a tube.
  • the wall thickness of the hose can be regulated by an axial movement of the control rod 27.
  • the outlet speed is regulated by the throttle screw 39.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Seal Device For Vehicle (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
EP89810907A 1988-12-09 1989-11-28 Tête d'extrusion Expired - Lifetime EP0373115B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT89810907T ATE73384T1 (de) 1988-12-09 1989-11-28 Extrusionskopf.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH456288 1988-12-09
CH4562/88 1988-12-09

Publications (2)

Publication Number Publication Date
EP0373115A1 true EP0373115A1 (fr) 1990-06-13
EP0373115B1 EP0373115B1 (fr) 1992-03-11

Family

ID=4278389

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89810907A Expired - Lifetime EP0373115B1 (fr) 1988-12-09 1989-11-28 Tête d'extrusion

Country Status (4)

Country Link
EP (1) EP0373115B1 (fr)
AT (1) ATE73384T1 (fr)
DE (1) DE58900957D1 (fr)
ES (1) ES2030589T3 (fr)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0427685A2 (fr) * 1989-11-06 1991-05-15 AUTOMA S.p.A. Tête d'extrusion permettant l'extrusion de plusieurs paraisons à partir d'une seule extrudeuse
WO2001062472A1 (fr) * 2000-02-22 2001-08-30 Soplar Sa Dispositif et procede de fabrication de corps creux en plastique
EP1338401A1 (fr) * 2002-02-13 2003-08-27 Battenfeld Extrusionstechnik GmbH Ligne d'extrusion pour tubes avec profil d'entretrois du support de mandrin

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1142057B (de) * 1961-03-13 1963-01-03 Mannesmann Ag Maschine zum gleichzeitigen Herstellen von mehreren Rohren aus Kunststoff
FR1330757A (fr) * 1962-04-06 1963-06-28 Saint Gobain Filière d'extrusion à orifice variable pour machine à former des objets creux, notamment en matière plastique
FR1385115A (fr) * 1964-03-06 1965-01-08 Union Carbide Corp Procédé et appareil pour fabriquer des objets creux en matière thermoplastique
DE1806007A1 (de) * 1968-10-30 1970-05-21 Midland Ross Corp Extruder-Formkopf
DE1629511A1 (de) * 1966-12-20 1972-03-16 Kautex Werke Gmbh Spritzkopf zum Extrudieren von Hohlstraengen aus thermoplastischem Kunststoff sowie Verfahren unter Verwendung desselben
US3724986A (en) * 1970-10-07 1973-04-03 Monsanto Co Apparatus for protecting an extrusion head from over pressure
FR2180737A1 (en) * 1972-04-21 1973-11-30 Siemens Ag Extrusion sheathing die - with flow rates to each of many dies independently balanced
US3801254A (en) * 1971-01-04 1974-04-02 Kautex Werke Gmbh Apparatus for making tubular parisons of thermoplastic material
EP0298908A1 (fr) * 1987-07-08 1989-01-11 Soplar Sa Dispositif de coextrusion
WO1989004247A1 (fr) * 1987-11-09 1989-05-18 Amelia Pessina Procede de production de feuilles thermoplastiques renforcees et appareil associe

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1142057B (de) * 1961-03-13 1963-01-03 Mannesmann Ag Maschine zum gleichzeitigen Herstellen von mehreren Rohren aus Kunststoff
FR1330757A (fr) * 1962-04-06 1963-06-28 Saint Gobain Filière d'extrusion à orifice variable pour machine à former des objets creux, notamment en matière plastique
FR1385115A (fr) * 1964-03-06 1965-01-08 Union Carbide Corp Procédé et appareil pour fabriquer des objets creux en matière thermoplastique
DE1629511A1 (de) * 1966-12-20 1972-03-16 Kautex Werke Gmbh Spritzkopf zum Extrudieren von Hohlstraengen aus thermoplastischem Kunststoff sowie Verfahren unter Verwendung desselben
DE1806007A1 (de) * 1968-10-30 1970-05-21 Midland Ross Corp Extruder-Formkopf
US3724986A (en) * 1970-10-07 1973-04-03 Monsanto Co Apparatus for protecting an extrusion head from over pressure
US3801254A (en) * 1971-01-04 1974-04-02 Kautex Werke Gmbh Apparatus for making tubular parisons of thermoplastic material
FR2180737A1 (en) * 1972-04-21 1973-11-30 Siemens Ag Extrusion sheathing die - with flow rates to each of many dies independently balanced
EP0298908A1 (fr) * 1987-07-08 1989-01-11 Soplar Sa Dispositif de coextrusion
WO1989004247A1 (fr) * 1987-11-09 1989-05-18 Amelia Pessina Procede de production de feuilles thermoplastiques renforcees et appareil associe

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN, Band 7, Nr. 47 (M-196)[1192], 24. Februar 1983; & JP-A-57 197 129 (SEKISUI KAGAKU KOGYO K.K.) 03-12-1982 *
PATENT ABSTRACTS OF JAPAN, Band 8, Nr. 258 (M-340)[1695], 27. November 1984; & JP-A-59 131 433 (TAKIRON K.K.) 28-07-1984 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0427685A2 (fr) * 1989-11-06 1991-05-15 AUTOMA S.p.A. Tête d'extrusion permettant l'extrusion de plusieurs paraisons à partir d'une seule extrudeuse
EP0427685A3 (fr) * 1989-11-06 1991-07-17 AUTOMA S.p.A. Tête d'extrusion permettant l'extrusion de plusieurs paraisons à partir d'une seule extrudeuse
WO2001062472A1 (fr) * 2000-02-22 2001-08-30 Soplar Sa Dispositif et procede de fabrication de corps creux en plastique
US6936198B2 (en) 2000-02-22 2005-08-30 Soplar Sa Device and method for producing hollow plastic bodies
EP1338401A1 (fr) * 2002-02-13 2003-08-27 Battenfeld Extrusionstechnik GmbH Ligne d'extrusion pour tubes avec profil d'entretrois du support de mandrin

Also Published As

Publication number Publication date
ES2030589T3 (es) 1992-11-01
EP0373115B1 (fr) 1992-03-11
DE58900957D1 (de) 1992-04-16
ATE73384T1 (de) 1992-03-15

Similar Documents

Publication Publication Date Title
DE2733913C2 (de) Verfahren und Vorrichtung zum Herstellen eines mehrschichtigen Spritzgußkörpers aus thermoplastischen Kunstharzen
DE2718537C3 (de) Extrudiereinrichtung zum Herstellen eines aus wenigstens zwei Schichten bestehenden Verbundrohres aus thermoplastischen Kunsts
DE1233571B (de) Verfahren und Vorrichtung zum Durchfuehren plastischen Materials von einer Plastifiziereinrichtung durch einen Durchflusskopf zu einer Duese zum Auspressen eines Stranges, insbesondere zum Herstellen eines Hohlkoerpers aus thermoplastischem Kunststoff nach dem Blasverfahren
EP0995579A2 (fr) Procédé de production en continu d'un tube composite avec manchon, et appareil pour la mise en oeuvre du procédé
DE102013105749B4 (de) Extrusionsschlauchkopf für diskontinuierliches Schäumen
DE2303583A1 (de) Verfahren zum herstellen von langgestreckten elementen, die im wesentlichen aus thermoplastischen polymerischen zusammensetzungen bestehen und als spitzen in schreibzeugen benutzt werden
DE3305242A1 (de) Pinole fuer den dorn eines schlauchkopfes zur herstellung von schlauchabschnitten oder schlaeuchen aus thermoplastischem kunststoff
DE1261657B (de) Spritzkopf zum Herstellen von schlauchfoermigen Straengen
DE1704791A1 (de) Vorrichtung zum Herstellen von im Querschnitt ringfoermigen Koerpern aus thermoplastischem Material
EP0373115B1 (fr) Tête d'extrusion
DE1274338B (de) Strangpresskopf zur Herstellung von rohrfoermigen Pressteilen aus thermoplastischem Material
DE2202200A1 (de) Press- und Spritzmaschine und Verfahren zur Herstellung von Formteilen
DE2754738A1 (de) Extrusionskopf
DE2625786C3 (de) Strangpreßkopf zum Herstellen eines Hohlstranges aus thermoplastischem Werkstoff
AT391294B (de) Spritzgussduese
DE1139970B (de) Umlenk-Spritzkopf fuer Schneckenpressen
DE1298698B (de) Vorrichtung zur Herstellung von schlauchfoermigen Filmen aus geschmolzenem thermoplastischem Material
DE2461340A1 (de) Spritzkopf zur erzeugung von zwei rohrfoermigen hohlstraengen aus thermoplastischem kunststoff
DE4204201C2 (de) Innenkühlvorrichtung für extrudierte Kunststoffschlauchfolien
DE2911572C2 (fr)
DE2232774A1 (de) Verfahren und vorrichtung zur herstellung eines folienschlauches aus kunststoff
DE4200628C1 (en) Extruder head with e.g. three settings - has die and intermediate feed tool which can both be rotated to align their angled flow bores differently with that supplied from extruder
DE2554238A1 (de) Werkzeug zum steglosen extrudieren von hohlprofilen
DE102021118705A1 (de) Vorrichtung und Verfahren für die biaxiale Kunststoff-Extrusion
DE2517254C3 (de) Vorrichtung zur Texturierung von in Ein- oder Mehrzahl vorliegenden synthetischen Endlosfäden mit einer Düse

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE

17P Request for examination filed

Effective date: 19900722

17Q First examination report despatched

Effective date: 19910301

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19920311

Ref country code: NL

Effective date: 19920311

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 19920311

REF Corresponds to:

Ref document number: 73384

Country of ref document: AT

Date of ref document: 19920315

Kind code of ref document: T

REF Corresponds to:

Ref document number: 58900957

Country of ref document: DE

Date of ref document: 19920416

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)
ITF It: translation for a ep patent filed

Owner name: ING. C. GREGORJ S.P.A.

ET Fr: translation filed
NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2030589

Country of ref document: ES

Kind code of ref document: T3

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19921130

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19981125

Year of fee payment: 10

Ref country code: FR

Payment date: 19981125

Year of fee payment: 10

Ref country code: AT

Payment date: 19981125

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 19981130

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19981203

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19981209

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19981215

Year of fee payment: 10

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991128

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991128

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991129

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991130

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991130

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19991130

BERE Be: lapsed

Owner name: S.A. SOPLAR

Effective date: 19991130

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19991128

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20000731

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20000901

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20001214

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 20051128